工业水处理 ›› 2008, Vol. 28 ›› Issue (4): 68-71. doi: 10.11894/1005-829x.2008.28(04).68

• 经验交流 • 上一篇    下一篇

反渗透系统后置离子交换床运行状态及分析

莫庆时   

  1. 广州半导体材料研究所, 广东广州 510610
  • 收稿日期:2007-12-28 出版日期:2008-04-20 发布日期:2010-10-01
  • 作者简介:莫庆时(1945- ), 高级工程师, 从事膜法水处理技术的设计研究, 电话: 020-87222754, E-mail: xklily@21cn.com。

Running s tate of follow-up ion exchange bed in RO sys tem and analys is

Mo Qingshi   

  1. Guangzhou Semiconductor Material Research Institute, Guangzhou 510610, China
  • Received:2007-12-28 Online:2008-04-20 Published:2010-10-01

摘要:

根据反渗透产水的特点,提出了按反渗透产水的总可交换阴离子与总可交换阳离子的比例来确定反渗透后置混床阴、阳树脂的配比,并对反渗透系统后设置脱气塔,后置阴床的OH-的累积、漏Na+等问题作了分析。

关键词: 水处理, 反渗透系统, 离子交换, 混床

Abstract:

Based on the characteristic of RO produced water, and according to the proportion of the total exchangeable anion (TEA) and total exchangeable cation (TEC) of RO produced water, the ratio of anion and cation resins in RO follow-up mixed bed has been determined. The problems, such as RO system follow-up degasifying column, hydroxide radical accumulation of the follow-up anion bed, Na+ leakage, etc. are analysed.

Key words: water treatment, reverse osmosis system, ion-exchange, mixed bed

中图分类号: